CA2269462A1 - Hydrocarbon gas processing - Google Patents
Hydrocarbon gas processingInfo
- Publication number
- CA2269462A1 CA2269462A1 CA002269462A CA2269462A CA2269462A1 CA 2269462 A1 CA2269462 A1 CA 2269462A1 CA 002269462 A CA002269462 A CA 002269462A CA 2269462 A CA2269462 A CA 2269462A CA 2269462 A1 CA2269462 A1 CA 2269462A1
- Authority
- CA
- Canada
- Prior art keywords
- stream
- distillation column
- distillation
- directed
- components
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000004215 Carbon black (E152) Substances 0.000 title abstract 4
- 229930195733 hydrocarbon Natural products 0.000 title abstract 4
- 150000002430 hydrocarbons Chemical class 0.000 title abstract 4
- 238000004821 distillation Methods 0.000 abstract 6
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 abstract 2
- 239000007788 liquid Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000001294 propane Substances 0.000 abstract 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 abstract 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 abstract 1
- 238000011084 recovery Methods 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/005—Processes comprising at least two steps in series
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C9/00—Aliphatic saturated hydrocarbons
- C07C9/02—Aliphatic saturated hydrocarbons with one to four carbon atoms
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0204—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
- F25J3/0209—Natural gas or substitute natural gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0204—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the feed stream
- F25J3/0219—Refinery gas, cracking gas, coke oven gas, gaseous mixtures containing aliphatic unsaturated CnHm or gaseous mixtures of undefined nature
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0233—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 1 carbon atom or more
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/0228—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream
- F25J3/0242—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream characterised by the separated product stream separation of CnHm with 3 carbon atoms or more
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/02—Processes or apparatus using separation by rectification in a single pressure main column system
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/50—Processes or apparatus using separation by rectification using multiple (re-)boiler-condensers at different heights of the column
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/78—Refluxing the column with a liquid stream originating from an upstream or downstream fractionator column
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
- F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/12—Refinery or petrochemical off-gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/02—Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. of the feed stream
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A process for the recovery of propane, propylene and heavier hydrocarbon components from a hydrocarbon gas stream is disclosed.
The stream is cooled and/or expanded to partially condense it, then separated to provide one or more C3 containing liquid streams and a first vapor stream. These streams are then directed into a distillation column wherein a second vapor stream is separated to recover a product containing the major portion of the C3 components and heavier hydrocarbon components. A distillation stream is withdrawn from the column below the feed point of the first vapor stream and is then directed into heat exchange relation with the second vapor stream to cool the distillation stream and condense at least a part of it, forming a condensed stream. At least a portion of the condensed stream is directed to the distillation column as its top feed. The quantities and temperatures of the feeds to the distillation column are effective to maintain the overhead temperature of the distillation column at a temperature whereby the major portion of the desired components is recovered.
The stream is cooled and/or expanded to partially condense it, then separated to provide one or more C3 containing liquid streams and a first vapor stream. These streams are then directed into a distillation column wherein a second vapor stream is separated to recover a product containing the major portion of the C3 components and heavier hydrocarbon components. A distillation stream is withdrawn from the column below the feed point of the first vapor stream and is then directed into heat exchange relation with the second vapor stream to cool the distillation stream and condense at least a part of it, forming a condensed stream. At least a portion of the condensed stream is directed to the distillation column as its top feed. The quantities and temperatures of the feeds to the distillation column are effective to maintain the overhead temperature of the distillation column at a temperature whereby the major portion of the desired components is recovered.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/738,321 US5799507A (en) | 1996-10-25 | 1996-10-25 | Hydrocarbon gas processing |
US08/738,321 | 1996-10-25 | ||
PCT/US1997/019340 WO1998017609A1 (en) | 1996-10-25 | 1997-10-24 | Hydrocarbon gas processing |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2269462A1 true CA2269462A1 (en) | 1998-04-30 |
CA2269462C CA2269462C (en) | 2001-04-10 |
Family
ID=24967510
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002269462A Expired - Lifetime CA2269462C (en) | 1996-10-25 | 1997-10-24 | Hydrocarbon gas processing |
Country Status (27)
Country | Link |
---|---|
US (1) | US5799507A (en) |
EP (1) | EP0937016B1 (en) |
JP (1) | JP3221570B2 (en) |
KR (1) | KR100415950B1 (en) |
CN (1) | CN1089740C (en) |
AR (1) | AR009393A1 (en) |
AT (1) | ATE204250T1 (en) |
AU (1) | AU728467B2 (en) |
BR (1) | BR9712373A (en) |
CA (1) | CA2269462C (en) |
CO (1) | CO4870777A1 (en) |
DE (1) | DE69706186T2 (en) |
DK (1) | DK0937016T3 (en) |
EA (1) | EA000813B1 (en) |
EG (1) | EG21661A (en) |
GE (1) | GEP20012499B (en) |
GT (1) | GT199700114A (en) |
ID (1) | ID19316A (en) |
MY (1) | MY116997A (en) |
NO (1) | NO325661B1 (en) |
NZ (1) | NZ335222A (en) |
PE (1) | PE75899A1 (en) |
SA (1) | SA98180785B1 (en) |
TW (1) | TW350021B (en) |
UA (1) | UA44869C2 (en) |
UY (1) | UY24761A1 (en) |
WO (1) | WO1998017609A1 (en) |
Families Citing this family (93)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6098425A (en) * | 1993-10-01 | 2000-08-08 | Stothers; William R. | Thermodynamic separation |
US6237365B1 (en) | 1998-01-20 | 2001-05-29 | Transcanada Energy Ltd. | Apparatus for and method of separating a hydrocarbon gas into two fractions and a method of retrofitting an existing cryogenic apparatus |
US6182469B1 (en) * | 1998-12-01 | 2001-02-06 | Elcor Corporation | Hydrocarbon gas processing |
US6311516B1 (en) * | 2000-01-27 | 2001-11-06 | Ronald D. Key | Process and apparatus for C3 recovery |
US6278035B1 (en) * | 2000-03-17 | 2001-08-21 | Ronald D. Key | Process for C2 recovery |
US6453698B2 (en) | 2000-04-13 | 2002-09-24 | Ipsi Llc | Flexible reflux process for high NGL recovery |
US6401486B1 (en) * | 2000-05-18 | 2002-06-11 | Rong-Jwyn Lee | Enhanced NGL recovery utilizing refrigeration and reflux from LNG plants |
WO2001088447A1 (en) * | 2000-05-18 | 2001-11-22 | Phillips Petroleum Company | Enhanced ngl recovery utilizing refrigeration and reflux from lng plants |
CN100451507C (en) * | 2000-10-02 | 2009-01-14 | 奥鲁工程有限公司 | Hydrocarbon gas processing |
US6712880B2 (en) | 2001-03-01 | 2004-03-30 | Abb Lummus Global, Inc. | Cryogenic process utilizing high pressure absorber column |
US6526777B1 (en) | 2001-04-20 | 2003-03-04 | Elcor Corporation | LNG production in cryogenic natural gas processing plants |
US6742358B2 (en) * | 2001-06-08 | 2004-06-01 | Elkcorp | Natural gas liquefaction |
UA76750C2 (en) * | 2001-06-08 | 2006-09-15 | Елккорп | Method for liquefying natural gas (versions) |
US6425266B1 (en) | 2001-09-24 | 2002-07-30 | Air Products And Chemicals, Inc. | Low temperature hydrocarbon gas separation process |
US6823692B1 (en) | 2002-02-11 | 2004-11-30 | Abb Lummus Global Inc. | Carbon dioxide reduction scheme for NGL processes |
US6931889B1 (en) * | 2002-04-19 | 2005-08-23 | Abb Lummus Global, Randall Gas Technologies | Cryogenic process for increased recovery of hydrogen |
CA2388266C (en) | 2002-05-30 | 2008-08-26 | Propak Systems Ltd. | System and method for liquefied petroleum gas recovery |
JP4193438B2 (en) | 2002-07-30 | 2008-12-10 | ソニー株式会社 | Manufacturing method of semiconductor device |
US6945075B2 (en) * | 2002-10-23 | 2005-09-20 | Elkcorp | Natural gas liquefaction |
US7069744B2 (en) * | 2002-12-19 | 2006-07-04 | Abb Lummus Global Inc. | Lean reflux-high hydrocarbon recovery process |
JP4571934B2 (en) * | 2003-02-25 | 2010-10-27 | オートロフ・エンジニアーズ・リミテッド | Hydrocarbon gas treatment |
US6889523B2 (en) | 2003-03-07 | 2005-05-10 | Elkcorp | LNG production in cryogenic natural gas processing plants |
US6662589B1 (en) | 2003-04-16 | 2003-12-16 | Air Products And Chemicals, Inc. | Integrated high pressure NGL recovery in the production of liquefied natural gas |
US7036337B2 (en) * | 2003-08-29 | 2006-05-02 | Wylie Companies, Inc | Recovery of hydrogen from refinery and petrochemical light ends streams |
US7155931B2 (en) * | 2003-09-30 | 2007-01-02 | Ortloff Engineers, Ltd. | Liquefied natural gas processing |
US7159417B2 (en) * | 2004-03-18 | 2007-01-09 | Abb Lummus Global, Inc. | Hydrocarbon recovery process utilizing enhanced reflux streams |
US7204100B2 (en) * | 2004-05-04 | 2007-04-17 | Ortloff Engineers, Ltd. | Natural gas liquefaction |
KR101200611B1 (en) * | 2004-07-01 | 2012-11-12 | 오르트로프 엔지니어스, 리미티드 | Liquefied natural gas processing |
RU2272973C1 (en) * | 2004-09-24 | 2006-03-27 | Салават Зайнетдинович Имаев | Method of low-temperature gas separation |
NZ556495A (en) * | 2005-02-24 | 2009-09-25 | Twister Bv | Method and system for cooling a natural gas stream and separating the cooled stream into various fractions |
US20070061950A1 (en) * | 2005-03-29 | 2007-03-22 | Terry Delonas | Lipowear |
CN101156038B (en) * | 2005-04-12 | 2010-11-03 | 国际壳牌研究有限公司 | Method and apparatus for liquefying a natural gas stream |
CA2619021C (en) * | 2005-04-20 | 2010-11-23 | Fluor Technologies Corporation | Integrated ngl recovery and lng liquefaction |
US9080810B2 (en) * | 2005-06-20 | 2015-07-14 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US20070261437A1 (en) * | 2006-05-12 | 2007-11-15 | Boonstra Eric F | Enhanced process for the purification of anhydrous hydrogen chloride gas |
CN101460800B (en) * | 2006-06-02 | 2012-07-18 | 奥特洛夫工程有限公司 | Liquefied natural gas processing |
WO2008008335A2 (en) * | 2006-07-10 | 2008-01-17 | Fluor Technologies Corporation | Configurations and methods for rich gas conditioning for ngl recovery |
JP2008050303A (en) * | 2006-08-24 | 2008-03-06 | Mitsubishi Chemicals Corp | Control method, control system and control program of distillation system |
US7777088B2 (en) * | 2007-01-10 | 2010-08-17 | Pilot Energy Solutions, Llc | Carbon dioxide fractionalization process |
US8590340B2 (en) * | 2007-02-09 | 2013-11-26 | Ortoff Engineers, Ltd. | Hydrocarbon gas processing |
US9869510B2 (en) * | 2007-05-17 | 2018-01-16 | Ortloff Engineers, Ltd. | Liquefied natural gas processing |
US8919148B2 (en) * | 2007-10-18 | 2014-12-30 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US9243842B2 (en) | 2008-02-15 | 2016-01-26 | Black & Veatch Corporation | Combined synthesis gas separation and LNG production method and system |
US8209997B2 (en) * | 2008-05-16 | 2012-07-03 | Lummus Technology, Inc. | ISO-pressure open refrigeration NGL recovery |
US20090282865A1 (en) | 2008-05-16 | 2009-11-19 | Ortloff Engineers, Ltd. | Liquefied Natural Gas and Hydrocarbon Gas Processing |
US20090293537A1 (en) * | 2008-05-27 | 2009-12-03 | Ameringer Greg E | NGL Extraction From Natural Gas |
US8584488B2 (en) * | 2008-08-06 | 2013-11-19 | Ortloff Engineers, Ltd. | Liquefied natural gas production |
US20100050688A1 (en) * | 2008-09-03 | 2010-03-04 | Ameringer Greg E | NGL Extraction from Liquefied Natural Gas |
MX341798B (en) * | 2009-02-17 | 2016-09-02 | Ortloff Engineers Ltd | Hydrocarbon gas processing. |
US9939195B2 (en) * | 2009-02-17 | 2018-04-10 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing including a single equipment item processing assembly |
US8881549B2 (en) * | 2009-02-17 | 2014-11-11 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US9074814B2 (en) * | 2010-03-31 | 2015-07-07 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US9080811B2 (en) * | 2009-02-17 | 2015-07-14 | Ortloff Engineers, Ltd | Hydrocarbon gas processing |
US9933207B2 (en) * | 2009-02-17 | 2018-04-03 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US9052136B2 (en) * | 2010-03-31 | 2015-06-09 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US9052137B2 (en) | 2009-02-17 | 2015-06-09 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US8434325B2 (en) | 2009-05-15 | 2013-05-07 | Ortloff Engineers, Ltd. | Liquefied natural gas and hydrocarbon gas processing |
US20100287982A1 (en) | 2009-05-15 | 2010-11-18 | Ortloff Engineers, Ltd. | Liquefied Natural Gas and Hydrocarbon Gas Processing |
EA201200006A1 (en) * | 2009-06-11 | 2012-05-30 | Ортлофф Инджинирс, Лтд. | HYDROCARBON GAS PROCESSING |
US20110067443A1 (en) * | 2009-09-21 | 2011-03-24 | Ortloff Engineers, Ltd. | Hydrocarbon Gas Processing |
US9021832B2 (en) | 2010-01-14 | 2015-05-05 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US9057558B2 (en) * | 2010-03-31 | 2015-06-16 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing including a single equipment item processing assembly |
US9068774B2 (en) * | 2010-03-31 | 2015-06-30 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US10113127B2 (en) | 2010-04-16 | 2018-10-30 | Black & Veatch Holding Company | Process for separating nitrogen from a natural gas stream with nitrogen stripping in the production of liquefied natural gas |
AU2011261670B2 (en) | 2010-06-03 | 2014-08-21 | Uop Llc | Hydrocarbon gas processing |
MY172490A (en) * | 2010-07-01 | 2019-11-27 | Black & Veatch Holding Co | Method and systems for recovering liquified petroleum gas from natural gas |
US8635885B2 (en) | 2010-10-15 | 2014-01-28 | Fluor Technologies Corporation | Configurations and methods of heating value control in LNG liquefaction plant |
WO2012075266A2 (en) | 2010-12-01 | 2012-06-07 | Black & Veatch Corporation | Ngl recovery from natural gas using a mixed refrigerant |
US10852060B2 (en) * | 2011-04-08 | 2020-12-01 | Pilot Energy Solutions, Llc | Single-unit gas separation process having expanded, post-separation vent stream |
KR101248232B1 (en) * | 2011-12-23 | 2013-03-27 | 재단법인 포항산업과학연구원 | Diagnosis method and system on deteriration of parallel driven utility equipments |
US10139157B2 (en) | 2012-02-22 | 2018-11-27 | Black & Veatch Holding Company | NGL recovery from natural gas using a mixed refrigerant |
CN104736504A (en) * | 2012-07-26 | 2015-06-24 | 氟石科技公司 | Configurations and methods for deep feed gas hydrocarbon dewpointing |
WO2014116273A1 (en) * | 2013-01-25 | 2014-07-31 | H R D Corporation | Method of high shear comminution of solids |
US9581385B2 (en) | 2013-05-15 | 2017-02-28 | Linde Engineering North America Inc. | Methods for separating hydrocarbon gases |
US9783470B2 (en) | 2013-09-11 | 2017-10-10 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
WO2015038288A1 (en) | 2013-09-11 | 2015-03-19 | Ortloff Engineers, Ltd. | Hydrocarbon processing |
AU2014318270B2 (en) | 2013-09-11 | 2018-04-19 | Uop Llc | Hydrocarbon gas processing |
US10563913B2 (en) | 2013-11-15 | 2020-02-18 | Black & Veatch Holding Company | Systems and methods for hydrocarbon refrigeration with a mixed refrigerant cycle |
US9574822B2 (en) | 2014-03-17 | 2017-02-21 | Black & Veatch Corporation | Liquefied natural gas facility employing an optimized mixed refrigerant system |
US10533794B2 (en) | 2016-08-26 | 2020-01-14 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US10551118B2 (en) | 2016-08-26 | 2020-02-04 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US10551119B2 (en) * | 2016-08-26 | 2020-02-04 | Ortloff Engineers, Ltd. | Hydrocarbon gas processing |
US11402155B2 (en) | 2016-09-06 | 2022-08-02 | Lummus Technology Inc. | Pretreatment of natural gas prior to liquefaction |
FR3066491B1 (en) * | 2017-05-18 | 2019-07-12 | Technip France | PROCESS FOR RECOVERING A C2 + HYDROCARBON CURRENT IN A REFINERY RESIDUAL GAS AND ASSOCIATED INSTALLATION |
US11428465B2 (en) | 2017-06-01 | 2022-08-30 | Uop Llc | Hydrocarbon gas processing |
US11543180B2 (en) | 2017-06-01 | 2023-01-03 | Uop Llc | Hydrocarbon gas processing |
US11015865B2 (en) | 2018-08-27 | 2021-05-25 | Bcck Holding Company | System and method for natural gas liquid production with flexible ethane recovery or rejection |
US11473837B2 (en) | 2018-08-31 | 2022-10-18 | Uop Llc | Gas subcooled process conversion to recycle split vapor for recovery of ethane and propane |
CA3132386A1 (en) | 2019-03-11 | 2020-09-17 | Uop Llc | Hydrocarbon gas processing |
US11643604B2 (en) | 2019-10-18 | 2023-05-09 | Uop Llc | Hydrocarbon gas processing |
EP4162217A1 (en) * | 2020-06-03 | 2023-04-12 | Chart Energy & Chemicals, Inc. | Gas stream component removal system and method |
US20230375263A1 (en) * | 2022-05-17 | 2023-11-23 | Gas Liquids Engineering Ltd. | Gas processing methodology utilizing reflux and additionally synthesized stream optimization |
US20230375265A1 (en) * | 2022-05-17 | 2023-11-23 | Gas Liquids Engineering Ltd. | Gas processing methodology utilizing reflux and additionally synthesized stream optimization |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4171964A (en) * | 1976-06-21 | 1979-10-23 | The Ortloff Corporation | Hydrocarbon gas processing |
US4157904A (en) * | 1976-08-09 | 1979-06-12 | The Ortloff Corporation | Hydrocarbon gas processing |
SU656648A1 (en) * | 1976-10-12 | 1979-04-15 | Всесоюзный научно-исследовательский институт природных газов | Method of separating hydrocarbon mixtures |
US4251249A (en) * | 1977-01-19 | 1981-02-17 | The Randall Corporation | Low temperature process for separating propane and heavier hydrocarbons from a natural gas stream |
US4278457A (en) * | 1977-07-14 | 1981-07-14 | Ortloff Corporation | Hydrocarbon gas processing |
USRE33408E (en) * | 1983-09-29 | 1990-10-30 | Exxon Production Research Company | Process for LPG recovery |
US4519824A (en) * | 1983-11-07 | 1985-05-28 | The Randall Corporation | Hydrocarbon gas separation |
FR2571129B1 (en) * | 1984-09-28 | 1988-01-29 | Technip Cie | PROCESS AND PLANT FOR CRYOGENIC FRACTIONATION OF GASEOUS LOADS |
US4617039A (en) * | 1984-11-19 | 1986-10-14 | Pro-Quip Corporation | Separating hydrocarbon gases |
US4687499A (en) * | 1986-04-01 | 1987-08-18 | Mcdermott International Inc. | Process for separating hydrocarbon gas constituents |
US4854955A (en) * | 1988-05-17 | 1989-08-08 | Elcor Corporation | Hydrocarbon gas processing |
US4869740A (en) * | 1988-05-17 | 1989-09-26 | Elcor Corporation | Hydrocarbon gas processing |
US4889545A (en) * | 1988-11-21 | 1989-12-26 | Elcor Corporation | Hydrocarbon gas processing |
US4895584A (en) * | 1989-01-12 | 1990-01-23 | Pro-Quip Corporation | Process for C2 recovery |
US5275005A (en) * | 1992-12-01 | 1994-01-04 | Elcor Corporation | Gas processing |
US5568737A (en) * | 1994-11-10 | 1996-10-29 | Elcor Corporation | Hydrocarbon gas processing |
WO1996040604A1 (en) * | 1995-06-07 | 1996-12-19 | Elcor Corporation | Hydrocarbon gas processing |
-
1996
- 1996-10-25 US US08/738,321 patent/US5799507A/en not_active Expired - Lifetime
-
1997
- 1997-10-24 BR BR9712373-0A patent/BR9712373A/en not_active IP Right Cessation
- 1997-10-24 EP EP97946304A patent/EP0937016B1/en not_active Expired - Lifetime
- 1997-10-24 DE DE69706186T patent/DE69706186T2/en not_active Expired - Lifetime
- 1997-10-24 WO PCT/US1997/019340 patent/WO1998017609A1/en active IP Right Grant
- 1997-10-24 AT AT97946304T patent/ATE204250T1/en not_active IP Right Cessation
- 1997-10-24 MY MYPI97005016A patent/MY116997A/en unknown
- 1997-10-24 KR KR10-1999-7003549A patent/KR100415950B1/en not_active IP Right Cessation
- 1997-10-24 UA UA99052835A patent/UA44869C2/en unknown
- 1997-10-24 GE GEAP19974762A patent/GEP20012499B/en unknown
- 1997-10-24 JP JP51966598A patent/JP3221570B2/en not_active Expired - Fee Related
- 1997-10-24 NZ NZ335222A patent/NZ335222A/en not_active IP Right Cessation
- 1997-10-24 CN CN97199161A patent/CN1089740C/en not_active Expired - Fee Related
- 1997-10-24 DK DK97946304T patent/DK0937016T3/en active
- 1997-10-24 CA CA002269462A patent/CA2269462C/en not_active Expired - Lifetime
- 1997-10-24 GT GT199700114A patent/GT199700114A/en unknown
- 1997-10-24 AU AU51503/98A patent/AU728467B2/en not_active Expired
- 1997-10-24 EA EA199900405A patent/EA000813B1/en not_active IP Right Cessation
- 1997-10-25 EG EG112497A patent/EG21661A/en active
- 1997-10-27 UY UY24761A patent/UY24761A1/en not_active IP Right Cessation
- 1997-10-27 PE PE1997000958A patent/PE75899A1/en not_active IP Right Cessation
- 1997-10-27 ID IDP973531A patent/ID19316A/en unknown
- 1997-10-27 AR ARP970104968A patent/AR009393A1/en active IP Right Grant
- 1997-10-27 CO CO97062829A patent/CO4870777A1/en unknown
- 1997-12-04 TW TW086118252A patent/TW350021B/en not_active IP Right Cessation
-
1998
- 1998-01-14 SA SA98180785A patent/SA98180785B1/en unknown
-
1999
- 1999-04-23 NO NO19991955A patent/NO325661B1/en not_active IP Right Cessation
Also Published As
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2269462A1 (en) | Hydrocarbon gas processing | |
CA2223042A1 (en) | Hydrocarbon gas processing | |
CA2003197A1 (en) | Hydrocarbon gas processing | |
CA2286117A1 (en) | Hydrocarbon gas processing | |
CA2204264A1 (en) | Hydrocarbon gas processing | |
MXPA05008280A (en) | Hydrocarbon gas processing. | |
CA2176184A1 (en) | Hydrocarbon gas processing | |
CA2351423A1 (en) | Hydrocarbon gas processing | |
WO2000031214A3 (en) | Recovery of propylene and ethylene from offgases | |
CA2423699A1 (en) | Hydrocarbon gas processing | |
CA2286112A1 (en) | Process for separating hydrocarbon gas constituents | |
CA1166145A (en) | Process to remove nitrogen from natural gas | |
MY157917A (en) | Hydrocarbon gas processing | |
KR950032026A (en) | Condensation-absorption complex olefin recovery | |
MY151033A (en) | Hydrocarbon gas processing | |
KR860001999A (en) | Ultra high purity oxygen production method | |
ES8608144A1 (en) | Air separation process. | |
US4529413A (en) | Recovering dessicant-antifreeze from admixture with water and hydrogen sulfide | |
KR970011765A (en) | How to separate ultra high purity oxygen from cryogenic air separation plant | |
EP1368604B1 (en) | Advanced heat integrated rectifier system | |
CA2363070C (en) | Impurities separation by distillation | |
US4299667A (en) | Process for recovering pure benzene | |
MX9709507A (en) | Hydrocarbon gas processing. | |
NZ207055A (en) | An apparatus and method for the recovery of light hydrocarbons from light hydrocarbon containing gases | |
ECSP972292A (en) | HYDROCARBON GAS PROCEDURE |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKEX | Expiry |
Effective date: 20171024 |